Patent classifications
B01D2255/92
Heat exchanger of an air-conditioning system of a cabin of an aircraft, and system comprising such a heat exchanger
Heat exchanger of an air-conditioning system of a cabin of a transport vehicle, comprising: a primary circuit supplied by a first air flow, a secondary circuit supplied by a second air flow, a casing defining an air-circulation enclosure, a primary circuit inlet box allowing entry into said air-circulation enclosure, and a primary circuit outlet box allowing exit from the air-circulation enclosure, characterized in that said inlet box is mounted removably on said casing, and in that it houses a three-dimensional structure forming a catalytic and/or adsorbent support for treating the air of said primary circuit, and a means for distributing said first air flow into said heat-exchange matrix.
CLOSED-ENVIRONMENT AIR PURIFICATION SYSTEM
An article includes a closed-environment air purification system that has a purifier through which air can be recirculated. The purifier is capable at a temperature of equal or less than 35 C. of converting hydrogen in the air to water and converting carbon monoxide in the air to carbon dioxide. The purifier has a reactor bed that includes media comprised of support particles and a metal catalyst disposed on the support particles.
COPPER-PROMOTED GMELINITE AND USE THEREOF IN THE SELECTIVE CATALYTIC REDUCTION OF NOX
A catalyst for the selective catalytic reduction of NOx comprises a zeolitic material which comprises (A) one or more zeolites having a GME framework structure containing YO.sub.2 and X.sub.2O.sub.3, and optionally further comprises one or more zeolites having a CHA framework structure containing YO.sub.2 and X.sub.2O.sub.3, and/or comprises, (B) one or more zeolite intergrowth phases of one or more zeolites having a GME framework structure containing YO.sub.2 and X.sub.2O.sub.3 and one or more zeolites having a CHA framework structure containing YO.sub.2 and X.sub.2O.sub.3, wherein Y is a tetravalent element, and X is a trivalent element, and the zeolitic material contains Cu and/or Fe as non-framework elements in an amount ranging from 0.1 to 15 wt. % calculated as the element and based on 100 wt. % of YO contained in the zeolitic material. Also provided are a process for its preparation, and a use in a method for the selective catalytic reduction of NOx.
Catalyst coatings incorporating binder compositions
Disclosed in certain implementations is a catalysis composition that includes a metal catalyst and a support material impregnated with the metal catalyst.
Exhaust gas purification catalyst and production method thereof
An exhaust gas purification catalyst contains an oxide 1 and an oxide 2. The catalyst has pores P.sub.1-260 with a pore size of from 1 nm to 260 nm, that can be measured by the nitrogen absorption method, and the total sum PV.sub.1-260 of the pore volume PV.sub.1-260 of the pores is equal to or greater than 0.79 cm.sup.3/g. The oxide 1 is an oxide with an oxygen release capability. The oxide 2 is represented by La.sub.xM.sub.1-xMO.sub.3- (2), where M is at least one element selected from the group consisting of Ba, Sr and Ca, M is at least one element selected from the group consisting of Fe, Co, Ni and Mn, is the amount of oxygen deficiency, x satisfies 0x1, and satisfies 01.
Honeycomb core for carrying catalyst and catalytic converter
A honeycomb core for carrying a catalyst includes a flat metal foil and a corrugated metal foil, which are layered. The corrugated foil is configured by repeating a concavo-convex shaped part including a first top surface that is in contact with one of the flat foils, a second top surface that is in contact with another flat foil and is disposed at a position where the second top surface avoids the first top surface, and an inclined leg surface that has one end connected to the first top surface through a first bent part and another end connected to the second top surface through a second bent part, and extends in a direction inclined with respect to the first top surface and the second top surface, and has an offset part having different wave phases between front and rear in an axial direction of the honeycomb core.
Monolithic composite photocatalysts
Monolithic composite photocatalysts for fluid purification are disclosed. The monolithic composite photocatalysts comprise a photoactive nanocrystal component and a non-photoactive porous support. Photocatalytic fluid purification systems that contact an impurity-containing fluid with the subject monolithic composite photocatalysts are also disclosed. The monolithic composite photocatalysts may be affixed to or embedded in scaffold structures to promote fluid flow through a fluid purification system and contact with the monolithic composite photocatalysts.
Catalyst modules and applications thereof
In one aspect, catalyst modules and catalytic reactors are provided which, in some embodiments, mitigate inefficiencies and/or problems associated with fluid stream pressure drop A catalyst module comprises a layer of structural catalyst bodies arranged in a pleated format, the structural catalyst bodies forming pleat inlet faces and pleat outlet faces, wherein fluid flow channels defined by inner partition walls of the structural catalyst bodies extend from the pleat inlet faces to the pleat outlet faces. The pleat inlet faces form an angle () with an inlet face of the module.
PARTICULATE FILTERS
The disclosure generally relates to filters, methods, and systems for filtering particulates from the exhaust of internal combustion engines such as gasoline direct injection engines and methods of preparing particulate filters.
Composition based on zirconium oxide and on at least one oxide of a rare earth other than cerium, having a specific porosity, processes for preparing same and use thereof in catalysis
A composition of zirconium oxide and at least one oxide of a rare earth other than cerium is described. The zirconium oxide has a weight proportion of at least 50% and, after calcination at a temperature of 900? C. for 4 hours, the composition exhibits two populations of pores of which their respective diameters are centered. The diameter of the first pore has a value of from 20 nm to 40 nm and in the second pore has a value of from 80 nm to 200 nm. Further described is how the composition can be used for treating the exhaust gases of internal combustion engines.